CN107062296A - One kind prevents station boiler low-temperature corrosion system - Google Patents
One kind prevents station boiler low-temperature corrosion system Download PDFInfo
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- CN107062296A CN107062296A CN201710196661.XA CN201710196661A CN107062296A CN 107062296 A CN107062296 A CN 107062296A CN 201710196661 A CN201710196661 A CN 201710196661A CN 107062296 A CN107062296 A CN 107062296A
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- air preheater
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- economizer
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- 238000005260 corrosion Methods 0.000 title claims abstract description 38
- 230000007797 corrosion Effects 0.000 title claims abstract description 38
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 162
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 81
- 239000003546 flue gas Substances 0.000 claims abstract description 81
- 239000007789 gas Substances 0.000 claims abstract description 77
- 238000010438 heat treatment Methods 0.000 claims abstract description 74
- 238000000034 method Methods 0.000 claims abstract description 9
- 239000002253 acid Substances 0.000 claims abstract description 8
- 238000001816 cooling Methods 0.000 claims description 36
- 238000006392 deoxygenation reaction Methods 0.000 claims description 26
- 230000001105 regulatory effect Effects 0.000 claims description 21
- 238000002485 combustion reaction Methods 0.000 claims description 20
- 229920006395 saturated elastomer Polymers 0.000 claims description 20
- 238000002156 mixing Methods 0.000 claims description 18
- 238000001704 evaporation Methods 0.000 claims description 12
- 230000008020 evaporation Effects 0.000 claims description 12
- 230000005611 electricity Effects 0.000 claims description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 7
- 229910052760 oxygen Inorganic materials 0.000 claims description 7
- 239000001301 oxygen Substances 0.000 claims description 7
- 239000008400 supply water Substances 0.000 claims description 7
- 239000000284 extract Substances 0.000 claims description 5
- 235000019504 cigarettes Nutrition 0.000 claims description 2
- 238000003303 reheating Methods 0.000 claims description 2
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 239000003245 coal Substances 0.000 description 9
- 239000000779 smoke Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical group [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- CUZMQPZYCDIHQL-VCTVXEGHSA-L calcium;(2s)-1-[(2s)-3-[(2r)-2-(cyclohexanecarbonylamino)propanoyl]sulfanyl-2-methylpropanoyl]pyrrolidine-2-carboxylate Chemical compound [Ca+2].N([C@H](C)C(=O)SC[C@@H](C)C(=O)N1[C@@H](CCC1)C([O-])=O)C(=O)C1CCCCC1.N([C@H](C)C(=O)SC[C@@H](C)C(=O)N1[C@@H](CCC1)C([O-])=O)C(=O)C1CCCCC1 CUZMQPZYCDIHQL-VCTVXEGHSA-L 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 239000003077 lignite Substances 0.000 description 1
- 210000003296 saliva Anatomy 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L15/00—Heating of air supplied for combustion
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D1/00—Feed-water heaters, i.e. economisers or like preheaters
- F22D1/36—Water and air preheating systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D1/00—Feed-water heaters, i.e. economisers or like preheaters
- F22D1/50—Feed-water heaters, i.e. economisers or like preheaters incorporating thermal de-aeration of feed-water
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Air Supply (AREA)
- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
Abstract
The invention discloses a kind of method for preventing station boiler low-temperature corrosion system and preventing station boiler low-temperature corrosion, cold air sends into the middle warm air preheater for being arranged in boiler back end ductwork after the hot water heating in air water air preheater, the tube wall temperature of warm air preheater is higher than flue gas acid dew point temperature in can improving, so as to avoid the low-temperature corrosion of air preheater；Flue gas feed-water heater is arranged after boiler back end ductwork air preheater to reduce exhaust gas temperature, simultaneously because into flue gas feed-water heater temperature at 100 DEG C or so, also it effectively prevent the low-temperature corrosion of flue gas feed-water heater, and whole unit heat is not increased and decreased, efficiency of generating unit is not interfered with.
Description
Technical field
The invention belongs to boiler plant field, and in particular to one kind prevents station boiler low-temperature corrosion system, more particularly to
A kind of high moisture content of burning, the Rear of Utility Boiler heating surface anti-low-temperature corrosion system of high-sulfur fuel.
Background technology
In station boiler（Including stratiform combustion, fluidized bed combustion, suspension combustion etc.）Burn high moisture content fuel, such as biomass, life
Rubbish living, sludge, coal slime, lignite etc., it may appear that high fume temperature, situation is more especially in HTHP and above parameter boiler
Seriously, for reduction exhaust gas temperature, the method generally used is that arrangement condenses water heater or in air preheat in back-end ductwork
Other additional heating surfaces etc. are arranged after device, though the above method can reduce exhaust gas temperature, help is had no to improving boiler thermal output.
Efficiency of generating unit can be influenceed to a certain degree using the method for condensation water heater, and arrange its Btu utilization of additional heating surface and be stranded
It is difficult.While final stage air preheater is low due to entering air temperature, especially in northern China winter, air preheater will be caused low
Temperature corrosion, although also have by using special substance to improve erosion resistance, but proved is limited.
In station boiler（Including stratiform combustion, fluidized bed combustion, suspension combustion etc.）Burning high sulfur part fuel, such as sulfur-rich coal, height
During sulphur coal etc., it may appear that serious low-temperature corrosion, especially in northern China winter, low-temperature corrosion of air preheater is more serious.
To solve the low-temperature corrosion of air preheater, being typically employed in before air preheater increases steam air heater, and increase air preheater enters
Mouth air themperature, but this also results in exhaust gas temperature rise, it is especially even more serious to high-ash fuel.
The content of the invention
It is an object of the invention to prevent station boiler low-temperature corrosion system by one kind, station boiler is solved（Including layer
Shape combustion, fluidized bed combustion, suspension combustion etc.）The low-temperature corrosion of final stage air preheater pipe, and improved for reduction exhaust gas temperature
Boiler thermal output and the final stage heating surface low-temperature corrosion problem occurred.
The technical scheme taken to achieve the above object of the present invention is：
Scheme one：A kind of system for preventing station boiler low-temperature corrosion, the high pressure and the above for more than 200 DEG C of feed temperature is solidifying
Vapour formula single reheat generating set, the system includes burner, burner hearth, superheater, drum collection vapour header, regulating valve, height
Warm economizer, high-temperature air preheater, low-level (stack-gas) economizer, middle warm air preheater, flue gas feed-water heater, air water air preheat
Device, blower fan, high-pressure heater, boiler feed pump, oxygen-eliminating device, low-pressure heater, condensate pump, condenser, steam turbine high-pressure cylinder,
Reheater and steam turbine mesolow cylinder, it is characterised in that：
Air enters air water air preheater by blower fan needed for burning, is heated to about 70 DEG C~100 DEG C, then by boiler flue
Interior middle warm air preheater and high-temperature air preheater, which are further heated to after hot blast design temperature, enters boiler combustion device；Combustion
Burn the flue gas produced and flow through burner hearth, superheater, reheater, high-temperature economizer, high-temperature air preheater, low-level (stack-gas) economizer, middle temperature
Discharged after air preheater, flue gas feed-water heater；Low-level (stack-gas) economizer, high-temperature economizer are passed through in feedwater of the temperature higher than 200 DEG C
The water entered after heating in drum, drum turns into saturated vapor by the heated evaporation of furnace wall cooling；The saturated vapor warp of generation
Superheater is heated to be the superheated steam with nominal parameter, and enters main steam line through collecting vapour header；Superheated steam passes through master
Jet chimney does work into steam turbine high-pressure cylinder, and the low pressure steam after steam turbine high-pressure cylinder acting introduces reheater and added again
Heat, plus thermogenetic high-temperature steam feeding steam turbine mesolow cylinder continue to do work；The condensed device cooling of exhaust steam after acting condenses,
Condensate is heated to after 145 DEG C~155 DEG C by condensate pump into low-pressure heater, is partly into air water air
Preheater heating cold air is cooled to 95 DEG C~105 DEG C, and the arranged flue gas in flue of the condensate after cooling, which feeds water, to be heated
Device is heated to sending into oxygen-eliminating device progress deoxygenation after 145 DEG C~155 DEG C, and another part is directly entered oxygen-eliminating device and carries out deoxygenation, passes through
Adjust the flow of both valve regulation；Deaerated water through boiler feed pump enter high-pressure heater be heated to more than 200 DEG C it is specified to
After coolant-temperature gage, low-level (stack-gas) economizer is sent into；Low-pressure heater draws gas heating from steam turbine mesolow cylinder；High-pressure heater is from steam turbine
High pressure cylinder draws gas heating；Oxygen-eliminating device is high pressure thermal deaerator, and extracting steam heating out from turbine low pressure cylinder carries out deoxygenation.
Scheme one is used for HTHP and above parameter station boiler condensing-type single reheat electricity generation system.
Scheme two：A kind of system for preventing station boiler low-temperature corrosion, high pressure for more than 200 DEG C of feed temperature and with
Upper condensing-type generating set, the system includes burner, burner hearth, superheater, drum collection vapour header, regulating valve, high temperature and saved
Coal device, high-temperature air preheater, low-level (stack-gas) economizer, middle warm air preheater, flue gas feed-water heater, air water air preheater,
Blower fan, high-pressure heater, boiler feed pump, oxygen-eliminating device, low-pressure heater, condensate pump, condenser, steam turbine, its feature exist
In：
Air enters air water air preheater by blower fan needed for burning, is heated to about 70 DEG C~100 DEG C, then by boiler flue
Interior middle warm air preheater and high-temperature air preheater, which are further heated to after hot blast design temperature, enters boiler combustion device；Combustion
Burn the flue gas produced and flow through burner hearth, superheater, high-temperature economizer, high-temperature air preheater, low-level (stack-gas) economizer, the preheating of middle warm air
Discharged after device, flue gas feed-water heater；Feedwater of the temperature higher than 200 DEG C is laggard by low-level (stack-gas) economizer, high-temperature economizer heating
The water entered in drum, drum turns into saturated vapor by the heated evaporation of furnace wall cooling；The saturated vapor of generation adds through superheater
Heat is the superheated steam with nominal parameter, and enters main steam line through collecting vapour header；Superheated steam passes through main steam line
Into steam turbine acting；The condensed device cooling of exhaust steam after acting condenses, and condensate enters low-pressure heater by condensate pump
It is heated to after 145 DEG C~155 DEG C, is partly into air water air preheater heating cold air and is cooled to 95 DEG C~105
DEG C, the arranged flue gas feed-water heater in flue of condensate after cooling sends into oxygen-eliminating device after being heated to 145 DEG C~155 DEG C
Deoxygenation is carried out, another part is directly entered oxygen-eliminating device and carries out deoxygenation, by the flow for adjusting both valve regulation；Deaerated water is through boiler
Feed pump is heated to after more than 200 DEG C of specified feed temperature into high-pressure heater, sends into low-level (stack-gas) economizer；Low-pressure heater
Drawn gas heating from steam turbine mesolow level；High-pressure heater draws gas heating from turbine high-pressure level；Oxygen-eliminating device is that high pressure heating power is removed
Oxygen device, extracts steam heating out from low-pressure stage of steam turbine and carries out deoxygenation.
Scheme two is used for HTHP and above parameter without reheating station boiler condensing-type electricity generation system.
Scheme three：One kind prevents station boiler low-temperature corrosion system, for 145 DEG C~155 DEG C of feed temperature high pressure with
Lower condensing generating set, the system includes burner, burner hearth, superheater, drum, collection vapour header, regulating valve, high temperature and saves coal
Device, high-temperature air preheater, low-level (stack-gas) economizer, middle warm air preheater, flue gas feed-water heater, air water air preheater, wind
Machine, high-pressure heater, boiler feed pump, oxygen-eliminating device, low-pressure heater, condensate pump, condenser, mixing header, steam turbine, its
It is characterised by：
Air needed for burning is heated to about 70 DEG C~100 DEG C by blower fan into air water air preheater, then by boiler flue
Interior middle warm air preheater and high-temperature air preheater, which are further heated to after hot blast design temperature, enters boiler combustion device；
It is pre- that the flue gas that burning is produced flows through burner hearth, superheater, high-temperature economizer, high-temperature air preheater, low-level (stack-gas) economizer, middle warm air
Discharged after hot device, flue gas feed-water heater；145 DEG C~155 DEG C of feedwater is by air water air preheater, flue gas feedwater heating
Enter drum after device, low-level (stack-gas) economizer, high-temperature economizer heating；Water in drum turns into full by the heated evaporation of furnace wall cooling
And steam；The saturated vapor of generation is heated to be the superheated steam with nominal parameter through superheater, and enters master through collecting vapour header
Jet chimney；Superheated steam is done work by main steam line into steam turbine, and the condensed device cooling of the exhaust steam after acting condenses, and coagulates
Bear water and entered by condensate pump after low-pressure heater heat temperature raising, deoxygenation is carried out into oxygen-eliminating device；Deaerated water is through boiler feedwater
Pump is heated to after 145 DEG C~155 DEG C into high-pressure heater, is partly into after air water air preheater heating cold air and is dropped
Temperature enters mixing header to 95 DEG C~105 DEG C after the arranged flue gas feed-water heater heating in flue of feedwater after cooling,
Another part is directly entered mixing header, and the control to temperature is realized by adjusting both valve regulation flow, mixed to give
Water introduces low-level (stack-gas) economizer；Low-pressure heater draws gas heating from steam turbine mesolow level；High-pressure heater from turbine high-pressure level
Draw gas heating；Oxygen-eliminating device is thermal deaerator, and extracting steam heating out from low-pressure stage of steam turbine carries out deoxygenation.
Scheme three is used for the following parameter station boiler condensing-type electricity generation system of high pressure, and feed temperature is 145 DEG C~155 DEG C
Scheme four：One kind prevents station boiler low-temperature corrosion system, for back pressure generating set, and the system includes burning and filled
Put, burner hearth, superheater, drum, collection vapour header, regulating valve, high-temperature economizer, high-temperature air preheater, low-level (stack-gas) economizer, middle temperature
It is air preheater, flue gas feed-water heater, air water air preheater, blower fan, high-pressure heater, boiler feed pump, oxygen-eliminating device, mixed
Intersection case, supply water heater, steam turbine, it is characterised in that：
Air needed for burning is heated to about 70 DEG C~100 DEG C by blower fan into air water air preheater, then by boiler flue
Interior middle warm air preheater and high-temperature air preheater, which are further heated to after hot blast design temperature, enters boiler combustion device；Combustion
Burn the flue gas produced and flow through burner hearth, superheater high-temperature economizer, high-temperature air preheater, low-level (stack-gas) economizer, the preheating of middle warm air
Discharged after device, flue gas feed-water heater；145 DEG C~155 DEG C of feedwater by air water air preheater, flue gas feed-water heater,
Enter drum after low-level (stack-gas) economizer, high-temperature economizer heating；Water in drum turns into saturation by the heated evaporation of furnace wall cooling
Steam；The saturated vapor of generation is heated to be the superheated steam with nominal parameter through superheater, and enters main steam through collecting vapour header
Steam pipe road；Superheated steam is done work by main steam line into steam turbine；A steam part after acting, which is delivered to, uses vapour unit,
Another part sends into oxygen-eliminating device；Oxygen-eliminating device is thermal deaerator；Feedwater is entered after supply water heater heating into oxygen-eliminating device
Row deoxygenation；After deaerated water is heated to about 150 DEG C through boiler feed pump into high-pressure heater, air water air preheat is partly into
95 DEG C~105 DEG C are cooled to after device heating Cryogenic air, the feedwater after cooling is arranged in the flue gas feed-water heater in flue
Enter mixing header after heating, another part is directly entered mixing header, realized by adjusting both valve regulation flow to temperature
The control of degree, mixed feedwater introduces low-level (stack-gas) economizer；High-pressure heater draws gas heating from turbine high-pressure level.
Scheme four is applied to back pressure type heat and power system, and feed temperature is 145 DEG C~155 DEG C.
System realizes the method for preventing station boiler low-temperature corrosion described in four schemes based on more than, it is characterised in that：
Cold wind enters in air water air preheater by blower fan, by 145 DEG C~155 DEG C of hot water heatings to about 70 DEG C~100
After DEG C, enter back into middle warm air preheater and further heat, higher temperature of inlet air and flue gas exit temperature, it is ensured that air
Preheater tube wall temperature is higher than the acid dew-point temperature of flue gas, it is to avoid the low-temperature corrosion of air preheater；For reduction exhaust gas temperature, carry
The thermal efficiency of high system, flue gas feed-water heater is designed with after middle warm air preheater, after air water air preheater is exchanged heat
Feedwater be heated to 145 DEG C~155 DEG C.Air water air preheater hot water outlet temperature be 95 DEG C~105 DEG C, enter back into flue gas to
Water heater, the higher inlet water temperature due to having, it is ensured that flue gas feed-water heater pipe wall temperature is higher than the acid dew point temperature of flue gas
Degree, it is to avoid low-temperature corrosion occurs for heating surface.Due to scheme one and scheme two enter the feedwater of air water air preheater for 145 DEG C~
155 DEG C, heating cold air cooling after, into flue gas feed-water heater by boiler smoke be reheated to 145 DEG C~155 DEG C it is laggard
Enter oxygen-eliminating device, do not lose and increase before and after the heat that feeds water, it has been mainly the function served as bridge of heat transfer, therefore does not interfere with
Efficiency of generating unit.
The solution have the advantages that：(1) cold air is carried out in air water air preheater by 150 DEG C or so of hot water
Preheating, is heated to about entering in smoke air preheater after 70 DEG C~100 DEG C, higher temperature of inlet air and exhanst gas outlet temperature
Degree, can effectively prevent the low-temperature corrosion of air preheater；(2) 150 DEG C or so of hot water quilt after air water air preheater is entered
100 DEG C or so are down to, flue gas feed-water heater is entered back into, the higher inlet water temperature due to having, it is ensured that flue gas feed-water heater
Pipe wall temperature is higher than the acid dew-point temperature of flue gas, it is to avoid low-temperature corrosion occurs for heating surface；(3) because flue gas feed-water heater enters
Exhaust gas temperature effectively can be reduced to less than 140 DEG C, improve boiler efficiency by saliva temperature at 100 DEG C or so；(4) 150 DEG C of heat
Water adds after cold air cooling, and 150 DEG C or so, whole unit heat are reheated to by boiler smoke into flue gas feed-water heater
Do not increase and decrease, do not interfere with efficiency of generating unit.
Brief description of the drawings
Fig. 1 is the system structure diagram of the present invention program one；
Fig. 2 is the system structure diagram of the present invention program two；
Fig. 3 is the system structure diagram of the present invention program three；
Fig. 4 is the system structure diagram of the present invention program four.
In figure：1. burner, 2. burner hearths, 3. superheaters, 4. drums, 5. collection vapour headers, 6. regulating valves, 7. high temperature are saved
Coal device, 8. high-temperature air preheaters, 9. low-level (stack-gas) economizers, warm air preheater, 11. flue gas feed-water heaters, 12. gas in 10.
Water air preheater, 13. blower fans, 14. high-pressure heaters, 15. boiler feed pumps, 16. oxygen-eliminating devices, 17. low-pressure heaters, 18.
Condensate pump, 19. condensers, 20. steam turbine high-pressure cylinders, 21. mixing headers, 22. supply water heaters, 23. reheaters, 24.
Steam turbine mesolow cylinder, 25. steam turbines.
Embodiment
Embodiment one：Illustrate with reference to Fig. 1, a kind of system for preventing station boiler low-temperature corrosion, for water temperature
The high pressure and above condensing-type single reheat generating set that more than 200 DEG C of degree, the system include burner 1, burner hearth 2, mistake
Hot device 3, drum 4, collection vapour header 5, regulating valve 6, high-temperature economizer 7, high-temperature air preheater 8, low-level (stack-gas) economizer 9, middle temperature are empty
Air preheater 10, flue gas feed-water heater 11, air water air preheater 12, blower fan 13, high-pressure heater 14, boiler feed pump
15th, in oxygen-eliminating device 16, low-pressure heater 17, condensate pump 18, condenser 19, steam turbine high-pressure cylinder 20, reheater 23, steam turbine
Low pressure (LP) cylinder 24.
Air enters air water air preheater 12 by blower fan 13 needed for burning, is heated to about 70 DEG C~100 DEG C, then pass through
Warm air preheater 10 and high-temperature air preheater 8, which are further heated to after hot blast design temperature, in boiler flue enters boiler
Burner 1；The flue gas that burning is produced flows through burner hearth 2, superheater 3, reheater 23, high-temperature economizer 7, high-temperature air preheater
8th, discharged after low-level (stack-gas) economizer 9, middle warm air preheater 10, flue gas feed-water heater 11；Feedwater of the temperature higher than 200 DEG C is passed through
The water that low-level (stack-gas) economizer 9, high-temperature economizer 7 enter in drum 4, drum after heating turns into by the heated evaporation of the water-cooling wall of burner hearth 2
Saturated vapor；The saturated vapor of generation is heated to be the superheated steam with nominal parameter through superheater 3, and enters through collecting vapour header 5
Enter main steam line；Superheated steam is done work by main steam line into steam turbine high-pressure cylinder 20, and steam turbine high-pressure cylinder 20 does work
Low pressure steam afterwards introduces reheater 23 and heated again, plus thermogenetic high-temperature steam feeding steam turbine mesolow cylinder 24 continues
Acting；The condensed cooling of device 19 of exhaust steam after acting is condensed, and condensate is heated by condensate pump 18 into low-pressure heater 17
It is warming up to after 150 DEG C or so, is partly into the heating cold air of air water air preheater 12 and is cooled to 100 DEG C or so, cooling
The arranged flue gas feed-water heater 11 in flue of condensate afterwards is heated to 150 DEG C or so rear feeding oxygen-eliminating devices 16 and removed
Oxygen, another part is directly entered oxygen-eliminating device 16 and carries out deoxygenation, and the flow of the two is adjusted by regulating valve 6；Deaerated water is given through boiler
Water pump 15 is heated to after more than 200 DEG C of specified feed temperature into high-pressure heater 14, sends into low-level (stack-gas) economizer 9；Low pressure adds
Hot device 17 draws gas heating from steam turbine mesolow cylinder 24；High-pressure heater 14 draws gas heating from steam turbine high-pressure cylinder 20；Oxygen-eliminating device
16 be high pressure thermal deaerator, and extracting steam heating out from the low pressure (LP) cylinder of steam turbine 20 carries out deoxygenation.
System described in present embodiment coagulates boiler in gas formula single reheat electricity generation system, the system for station boiler
The HTHP and the boiler of above parameter that more than 200 DEG C of feed temperature.
Embodiment two：Illustrate with reference to Fig. 2, a kind of system for preventing station boiler low-temperature corrosion, for water temperature
The high pressure and above condensing-type generating set that more than 200 DEG C of degree, the system include burner 1, burner hearth 2, superheater 3, pot
Cylinder 4, collection vapour header 5, regulating valve 6, high-temperature economizer 7, high-temperature air preheater 8, low-level (stack-gas) economizer 9, middle warm air preheater
10th, flue gas feed-water heater 11, air water air preheater 12, blower fan 13, high-pressure heater 14, boiler feed pump 15, oxygen-eliminating device
16th, low-pressure heater 17, condensate pump 18, condenser 19, steam turbine 25.
Air enters air water air preheater 12 by blower fan 13 needed for burning, is heated to about 70 DEG C~100 DEG C, then pass through
Warm air preheater 10 and high-temperature air preheater 8, which are further heated to after hot blast design temperature, in boiler flue enters boiler
Burner 1；The flue gas that burning is produced flows through burner hearth 2, superheater 3, high-temperature economizer 7, high-temperature air preheater 8, low temperature and saved
Discharged after coal device 9, middle warm air preheater 10, flue gas feed-water heater 11；Feedwater of the temperature higher than 200 DEG C saves coal by low temperature
The water that device 9, high-temperature economizer 7 enter in drum 4, drum after heating turns into saturated vapor by the heated evaporation of the water-cooling wall of burner hearth 2；
The saturated vapor of generation is heated to be the superheated steam with nominal parameter through superheater 3, and enters main steam pipe through collecting vapour header 5
Road；Superheated steam is done work by main steam line into steam turbine 25；The condensed cooling of device 19 of exhaust steam after acting condenses, and condenses
Water is heated to after 145 DEG C~155 DEG C by condensate pump 18 into low-pressure heater 17, is partly into air water air
The heating cold air of preheater 12 is cooled to 95 DEG C~105 DEG C, and the arranged flue gas feedwater in flue of the condensate after cooling adds
Hot device 11 is heated to sending into the progress deoxygenation of oxygen-eliminating device 16 after 145 DEG C~155 DEG C, and another part is directly entered oxygen-eliminating device 16 and removed
Oxygen, the flow of the two is adjusted by regulating valve 6；Deaerated water is heated to 200 DEG C through boiler feed pump 15 into high-pressure heater 14
After specified feed temperature above, low-level (stack-gas) economizer 9 is sent into；Low-pressure heater 17 draws gas heating from steam turbine 25 mesolow level；
High-pressure heater 14 is heated from the high-stage bleed of steam turbine 25；Oxygen-eliminating device 16 is high pressure thermal deaerator, from the low pressure of steam turbine 25
Level extracts steam heating out and carries out deoxygenation.
System described in present embodiment is that station boiler coagulates gas formula electricity generation system, and the system unit is without reheated steam system
System, boiler is the HTHP of more than 200 DEG C of feed temperature and the boiler of above parameter in the system.
Embodiment three：Illustrate with reference to Fig. 3, one kind prevents station boiler low-temperature corrosion system, for feed temperature
145 DEG C~155 DEG C of the following condensing generating set of high pressure, the system include burner 1, burner hearth 2, superheater 3, drum 4,
Collect vapour header 5, regulating valve 6, high-temperature economizer 7, high-temperature air preheater 8, low-level (stack-gas) economizer 9, middle warm air preheater 10, cigarette
It is gas feed-water heater 11, air water air preheater 12, blower fan 13, high-pressure heater 14, boiler feed pump 15, oxygen-eliminating device 16, low
Press heater 17, condensate pump 18, condenser 19, mixing header 21, steam turbine 25.
Air needed for burning enters air water air preheater 12 by blower fan 13 and is heated to about 70 DEG C~100 DEG C, then passes through
Middle warm air preheater 10 and high-temperature air preheater 8 in boiler flue, which are further heated to after hot blast design temperature, enters pot
Stove burner 1；The flue gas that burning is produced flows through burner hearth 2, superheater 3, high-temperature economizer 7, high-temperature air preheater 8, low temperature
Discharged after economizer 9, middle warm air preheater 10, flue gas feed-water heater 11；145 DEG C~155 DEG C of feedwater is empty by air water
Air preheater 12, flue gas feed-water heater 11, low-level (stack-gas) economizer 9, high-temperature economizer 7 enter drum 4 after heating；Water in drum
Turn into saturated vapor by the heated evaporation of the water-cooling wall of burner hearth 4；The saturated vapor of generation is heated to be with nominal parameter through superheater 3
Superheated steam, and through collect vapour header 5 enter main steam line；Superheated steam is done by main steam line into steam turbine 25
Work(, the condensed cooling of device 19 of exhaust steam after acting condenses, and condensate enters low-pressure heater 17 by condensate pump 18 and heats liter
Wen Hou, deoxygenation is carried out into oxygen-eliminating device 16；Deaerated water through boiler feed pump 15 into high-pressure heater 14 be heated to 145 DEG C~
After 155 DEG C, it is partly into after the heating cold air of air water air preheater 12 and is cooled to 95 DEG C~105 DEG C, giving after cooling
The arranged flue gas feed-water heater 11 in flue of water enters mixing header 21 after heating, another part is directly entered mixing collection
Case 21, the control to temperature is realized by the two flow of the regulation of regulating valve 6, and mixed feedwater introduces low-level (stack-gas) economizer 9；It is low
Pressure heater 17 draws gas heating from steam turbine 25 mesolow level；High-pressure heater 14 is heated from the high-stage bleed of steam turbine 25；Remove
Oxygen device 16 is thermal deaerator, and extracting steam heating out from the low-pressure stage of steam turbine 25 carries out deoxygenation.
System described in present embodiment is that station boiler coagulates gas formula electricity generation system, and 145 DEG C~155 DEG C of feed temperature
The following parameter boiler of high pressure.
Embodiment four：Illustrate with reference to Fig. 4, one kind prevents station boiler low-temperature corrosion system, generated electricity for back pressure
Unit, the system include burner 1, burner hearth 2, superheater 3, drum 4, collection vapour header 5, regulating valve 6, high-temperature economizer 7,
High-temperature air preheater 8, low-level (stack-gas) economizer 9, middle warm air preheater 10, flue gas feed-water heater 11, air water air preheater
12nd, blower fan 13, high-pressure heater 14, boiler feed pump 15, oxygen-eliminating device 16, mixing header 21, supply water heater 22, steam turbine
25。
Air needed for burning enters air water air preheater 12 by blower fan 13 and is heated to about 70 DEG C~100 DEG C, then passes through
Warm air preheater 10 and high-temperature air preheater 8, which are further heated to after hot blast design temperature, in boiler flue enters boiler
Burner 1；The flue gas that burning is produced flows through burner hearth 2, the high-temperature economizer 7 of superheater 3, high-temperature air preheater 8, low temperature and saves coal
Discharged after device 9, middle warm air preheater 10, flue gas feed-water heater 11；145 DEG C~155 DEG C of feedwater is pre- by air water air
Hot device 12, flue gas feed-water heater 11, low-level (stack-gas) economizer 9, high-temperature economizer 7 enter drum 4 after heating；Water in drum passes through
The heated evaporation of the water-cooling wall of burner hearth 4 turns into saturated vapor；The saturated vapor of generation is heated to be the mistake with nominal parameter through superheater 3
Vapours, and enter main steam line through collecting vapour header 5；Superheated steam is done work by main steam line into steam turbine 25；Do
A steam part after work(, which is delivered to, uses vapour unit, another part feeding oxygen-eliminating device 16；Oxygen-eliminating device 16 is thermal deaerator；Feedwater
Enter oxygen-eliminating device 16 after supply water heater 22 is heated and carry out deoxygenation；Deaerated water enters hyperbaric heating through boiler feed pump 15
Device 14 is heated to about after 150 DEG C, and 95 DEG C~105 are cooled to after being partly into the heating Cryogenic air of air water air preheater 12
DEG C, the arranged flue gas feed-water heater 11 in flue of feedwater after cooling enters mixing header 21, another part after heating
Mixing header 21 is directly entered, the control to temperature is realized by the two flow of the regulation of regulating valve 6, mixed feedwater is introduced
Low-level (stack-gas) economizer 9；High-pressure heater 14 is heated from the high-stage bleed of steam turbine 25.
System described in present embodiment is back pressure type electricity generation system, and the boiler of 145 DEG C~155 DEG C of feed temperature.
Applied to system described in above embodiment one, two, three or four station boiler low-temperature corrosion is prevented to realize
Method, methods described is：
Cold wind enters in air water air preheater 12 by blower fan 13, by 145 DEG C~155 DEG C of hot water heatings to about 70 DEG C~
After 100 DEG C, the further heating of middle warm air preheater 10 is entered back into, higher temperature of inlet air and flue gas exit temperature are protected
Demonstrate,prove the acid dew-point temperature that air preheater tube wall temperature is higher than flue gas, it is to avoid the low-temperature corrosion of air preheater；For reduction smoke evacuation
Temperature, the thermal efficiency for improving system, flue gas feed-water heater 11 is designed with after middle warm air preheater 10, and air water air is pre-
Feedwater after hot device 12 exchanges heat is heated to 145 DEG C~155 DEG C.The hot water outlet temperature of air water air preheater 12 is 95 DEG C~105
DEG C, flue gas feed-water heater 11 is entered back into, the higher inlet water temperature due to having, it is ensured that the pipe wall temperature of flue gas feed-water heater 11
Higher than the acid dew-point temperature of flue gas, it is to avoid low-temperature corrosion occurs for heating surface.Because scheme one and scheme two are pre- into air water air
The feedwater of hot device 12 be 145 DEG C~155 DEG C, plus cold air cooling after, into flue gas feed-water heater 11 by boiler smoke again
It is heated to after 145 DEG C~155 DEG C entering oxygen-eliminating device 16, does not lose and increase before and after the heat that feeds water, it has been mainly heat biography
The function served as bridge passed, therefore do not interfere with efficiency of generating unit.
Claims (5)
1. one kind prevents station boiler low-temperature corrosion system, for the high pressure and above condensing-type one of more than 200 DEG C of feed temperature
Secondary reheating generating set, the system includes burner（1）, burner hearth（2）, superheater（3）, drum（4）Collect vapour header（5）、
Regulating valve（6）, high-temperature economizer（7）, high-temperature air preheater（8）, low-level (stack-gas) economizer（9）, middle warm air preheater（10）, cigarette
Gas feed-water heater（11）, air water air preheater（12）, blower fan（13）, high-pressure heater（14）, boiler feed pump（15）, remove
Oxygen device（16）, low-pressure heater（17）, condensate pump（18）, condenser（19）, steam turbine high-pressure cylinder（20）, reheater（23）、
Steam turbine mesolow cylinder（24）, it is characterised in that：
Air needed for burning passes through blower fan（13）Into air water air preheater（12）, 70 DEG C~100 DEG C are heated to about, then pass through
Warm air preheater in boiler flue（10）And high-temperature air preheater（8）Enter after being further heated to hot blast design temperature
Boiler combustion device（1）；The flue gas that burning is produced flows through burner hearth（2）, superheater（3）, reheater（23）, high-temperature economizer（7）、
High-temperature air preheater（8）, low-level (stack-gas) economizer（9）, middle warm air preheater（10）, flue gas feed-water heater（11）After discharge；
Low-level (stack-gas) economizer is passed through in feedwater of the temperature higher than 200 DEG C（9）, high-temperature economizer（7）Enter drum after heating（4）, in drum
Water passes through burner hearth（2）The heated evaporation of water-cooling wall turns into saturated vapor；The saturated vapor of generation is through superheater（3）It is heated to be with volume
Determine the superheated steam of parameter, and through collecting vapour header（5）Into main steam line；Superheated steam enters steamer by main steam line
Machine high pressure cylinder（20）Acting, steam turbine high-pressure cylinder（20）Low pressure steam after acting introduces reheater（23）Heat again, plus
Thermogenetic high-temperature steam sends into steam turbine mesolow cylinder（24）Continue to do work；The condensed device of exhaust steam after acting（19）Cooling is solidifying
Knot, condensate passes through condensate pump（18）Into low-pressure heater（17）It is heated to after 145 DEG C~155 DEG C, a part
Into air water air preheater（12）Heating cold air is cooled to 95 DEG C~105 DEG C, and the condensate after cooling is arranged in flue
Interior flue gas feed-water heater（11）Oxygen-eliminating device is sent into after being heated to 145 DEG C~155 DEG C（16）Deoxygenation is carried out, another part is direct
Into oxygen-eliminating device（16）Deoxygenation is carried out, passes through regulating valve（6）Adjust the flow of the two；Deaerated water is through boiler feed pump（15）Into
High-pressure heater（14）It is heated to after more than 200 DEG C of specified feed temperature, sends into low-level (stack-gas) economizer（9）；Low-pressure heater
（17）From steam turbine mesolow cylinder（24）Draw gas heating；High-pressure heater（14）From steam turbine high-pressure cylinder（20）Draw gas heating；Remove
Oxygen device（16）For high pressure thermal deaerator, from steam turbine（20）Low pressure (LP) cylinder extracts steam heating out and carries out deoxygenation.
2. one kind prevents station boiler low-temperature corrosion system, high pressure and above condensing-type for more than 200 DEG C of feed temperature are sent out
Group of motors, the system includes burner（1）, burner hearth（2）, superheater（3）, drum（4）Collect vapour header（5）, regulating valve
（6）, high-temperature economizer（7）, high-temperature air preheater（8）, low-level (stack-gas) economizer（9）, middle warm air preheater（10）, flue gas feedwater
Heater（11）, air water air preheater（12）, blower fan（13）, high-pressure heater（14）, boiler feed pump（15）, oxygen-eliminating device
（16）, low-pressure heater（17）, condensate pump（18）, condenser（19）, steam turbine（25）, it is characterised in that：
Air needed for burning passes through blower fan（13）Into air water air preheater（12）, 70 DEG C~100 DEG C are heated to about, then pass through
Warm air preheater in boiler flue（10）And high-temperature air preheater（8）Enter after being further heated to hot blast design temperature
Boiler combustion device（1）；The flue gas that burning is produced flows through burner hearth（2）, superheater（3）, high-temperature economizer（7）, high temperature air it is pre-
Hot device（8）, low-level (stack-gas) economizer（9）, middle warm air preheater（10）, flue gas feed-water heater（11）After discharge；Temperature is higher than 200
DEG C feedwater pass through low-level (stack-gas) economizer（9）, high-temperature economizer（7）Enter drum after heating（4）, the water in drum passes through burner hearth
（2）The heated evaporation of water-cooling wall turns into saturated vapor；The saturated vapor of generation is through superheater（3）It is heated to be the mistake with nominal parameter
Vapours, and through collecting vapour header（5）Into main steam line；Superheated steam enters steam turbine by main steam line（25）Do
Work(；The condensed device of exhaust steam after acting（19）Cooling condenses, and condensate passes through condensate pump（18）Into low-pressure heater（17）
It is heated to after 145 DEG C~155 DEG C, is partly into air water air preheater（12）Heating cold air be cooled to 95 DEG C~
105 DEG C, the condensate after cooling is arranged in the flue gas feed-water heater in flue（11）Sent after being heated to 145 DEG C~155 DEG C
Enter oxygen-eliminating device（16）Deoxygenation is carried out, another part is directly entered oxygen-eliminating device（16）Deoxygenation is carried out, passes through regulating valve（6）Both regulations
Flow；Deaerated water is through boiler feed pump（15）Into high-pressure heater（14）It is heated to more than 200 DEG C of specified feed temperature
Afterwards, low-level (stack-gas) economizer is sent into（9）；Low-pressure heater（17）From steam turbine（25）Mesolow level is drawn gas heating；High-pressure heater
（14）From steam turbine（25）High-stage bleed is heated；Oxygen-eliminating device（16）For high pressure thermal deaerator, from steam turbine（25）Low-pressure stage
Extract steam heating out and carry out deoxygenation.
3. one kind prevents station boiler low-temperature corrosion system, condensing following for 145 DEG C~155 DEG C of high pressure of feed temperature generates electricity
Unit, the system includes burner（1）, burner hearth（2）, superheater（3）, drum（4）, collection vapour header（5）, regulating valve（6）、
High-temperature economizer（7）, high-temperature air preheater（8）, low-level (stack-gas) economizer（9）, middle warm air preheater（10）, flue gas feedwater heating
Device（11）, air water air preheater（12）, blower fan（13）, high-pressure heater（14）, boiler feed pump（15）, oxygen-eliminating device（16）、
Low-pressure heater（17）, condensate pump（18）, condenser（19）, mixing header（21）, steam turbine（25）, it is characterised in that：
Air needed for burning passes through blower fan（13）Into air water air preheater（12）70 DEG C~100 DEG C are heated to about, then is passed through
Middle warm air preheater in boiler flue（10）And high-temperature air preheater（8）It is further heated to hot blast design temperature laggard
Enter boiler combustion device（1）；The flue gas that burning is produced flows through burner hearth（2）, superheater（3）, high-temperature economizer（7）, high temperature air
Preheater（8）, low-level (stack-gas) economizer（9）, middle warm air preheater（10）, flue gas feed-water heater（11）After discharge；145 DEG C~
Air water air preheater is passed through in 155 DEG C of feedwater（12）, flue gas feed-water heater（11）, low-level (stack-gas) economizer（9）, high-temperature economizer
（7）Enter drum after heating（4）；Water in drum passes through burner hearth（4）The heated evaporation of water-cooling wall turns into saturated vapor；What is produced is full
With steam through superheater（3）It is heated to be the superheated steam with nominal parameter, and through collecting vapour header（5）Into main steam line；
Superheated steam enters steam turbine by main steam line（25）Acting, the condensed device of exhaust steam after acting（19）Cooling condenses, and coagulates
Bear water by condensate pump（18）Into low-pressure heater（17）After heat temperature raising, into oxygen-eliminating device（16）Carry out deoxygenation；Deoxygenation
Water is through boiler feed pump（15）Into high-pressure heater（14）It is heated to after 145 DEG C~155 DEG C, is partly into air water air
Preheater（12）95 DEG C~105 DEG C are cooled to after heating cold air, the feedwater after cooling is arranged in the flue gas feedwater in flue
Heater（11）Enter mixing header after heating（21）, another part is directly entered mixing header（21）, pass through regulating valve（6）Adjust
Save the two flow to realize the control to temperature, mixed feedwater introduces low-level (stack-gas) economizer（9）；Low-pressure heater（17）From vapour
Turbine（25）Mesolow level is drawn gas heating；High-pressure heater（14）From steam turbine（25）High-stage bleed is heated；Oxygen-eliminating device（16）
For thermal deaerator, from steam turbine（25）Low-pressure stage extracts steam heating out and carries out deoxygenation.
4. one kind prevents station boiler low-temperature corrosion system, for back pressure generating set, the system includes burner（1）、
Burner hearth（2）, superheater（3）, drum（4）, collection vapour header（5）, regulating valve（6）, high-temperature economizer（7）, high-temperature air preheater
（8）, low-level (stack-gas) economizer（9）, middle warm air preheater（10）, flue gas feed-water heater（11）, air water air preheater（12）, wind
Machine（13）, high-pressure heater（14）, boiler feed pump（15）, oxygen-eliminating device（16）, mixing header（21）, supply water heater
（22）, steam turbine（25）, it is characterised in that：
Air needed for burning passes through blower fan（13）Into air water air preheater（12）70 DEG C~100 DEG C are heated to about, then is passed through
Warm air preheater in boiler flue（10）And high-temperature air preheater（8）Enter after being further heated to hot blast design temperature
Boiler combustion device（1）；The flue gas that burning is produced flows through burner hearth（2）, superheater（3）High-temperature economizer（7）, high temperature air preheating
Device（8）, low-level (stack-gas) economizer（9）, middle warm air preheater（10）, flue gas feed-water heater（11）After discharge；145 DEG C~155 DEG C
Feedwater pass through air water air preheater（12）, flue gas feed-water heater（11）, low-level (stack-gas) economizer（9）, high-temperature economizer（7）Plus
Enter drum after heat（4）；Water in drum passes through burner hearth（4）The heated evaporation of water-cooling wall turns into saturated vapor；The saturation of generation is steamed
Vapour is through superheater（3）It is heated to be the superheated steam with nominal parameter, and through collecting vapour header（5）Into main steam line；Overheat
Steam enters steam turbine by main steam line（25）Acting；A steam part after acting, which is delivered to, uses vapour unit, another portion
It is distributed into oxygen-eliminating device（16）；Oxygen-eliminating device（16）For thermal deaerator；Feedwater is by supply water heater（22）Enter after heating and remove
Oxygen device（16）Carry out deoxygenation；Deaerated water is through boiler feed pump（15）Into high-pressure heater（14）It is heated to about after 150 DEG C, one
Divide and enter air water air preheater（12）Heating Cryogenic air after be cooled to 95 DEG C~105 DEG C, the feedwater after cooling it is arranged in
Flue gas feed-water heater in flue（11）Enter mixing header after heating（21）, another part is directly entered mixing header
（21）, pass through regulating valve（6）Adjust the two flow to realize the control to temperature, mixed feedwater introduces low-level (stack-gas) economizer
（9）；High-pressure heater（14）From steam turbine（25）High-stage bleed is heated.
5. the method for preventing station boiler low-temperature corrosion realized based on system described in claim 1,2,3 or 4, its feature is existed
In its method is：
Cold wind passes through blower fan（13）Into air water air preheater（12）In, by 145 DEG C~155 DEG C of hot water heatings to about 70
DEG C~100 DEG C after, enter back into middle warm air preheater（10）Further heating, higher temperature of inlet air and exhanst gas outlet temperature
Degree, it is ensured that air preheater tube wall temperature is higher than the acid dew-point temperature of flue gas, it is to avoid the low-temperature corrosion of air preheater；For reduction
Exhaust gas temperature, the thermal efficiency for improving system, in middle warm air preheater（10）After be designed with flue gas feed-water heater（11）, by gas
Water air preheater（12）Feedwater after heat exchange is heated to 145 DEG C~155 DEG C；Air water air preheater（12）Hot water outlet temperature
For 95 DEG C~105 DEG C, flue gas feed-water heater is entered back into（11）, the higher inlet water temperature due to having, it is ensured that flue gas feedwater adds
Hot device（11）Pipe wall temperature is higher than the acid dew-point temperature of flue gas, it is to avoid low-temperature corrosion occurs for heating surface.
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| CN108375060A (en) * | 2018-02-09 | 2018-08-07 | 浙江浙能龙泉生物质发电有限公司 | A kind of Steam Turbine Regenerative System and method using medium temperature flue gas condensed water |
| CN111536501A (en) * | 2020-05-09 | 2020-08-14 | 济南达能动力技术有限责任公司 | Heating method for boiler deaerator inlet water |
| CN112963819A (en) * | 2021-04-16 | 2021-06-15 | 西安热工研究院有限公司 | Steam-water system arrangement structure of deep peak regulation double-hearth power station pulverized coal boiler |
| CN114857610A (en) * | 2022-04-12 | 2022-08-05 | 光大环保（中国）有限公司 | Air preheating system and method for waste incineration power plant |
| CN117515517A (en) * | 2023-11-03 | 2024-02-06 | 中石化宁波工程有限公司 | Parallel electric heating type air supply boiler steam generating system |
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